Lignosulfonate-modified calcium hydroxide for SO2 control during furnace injection

ABSTRACT

A method is provided for removing sulphur-containing gases from fossil fuel-fired combustors comprising the step of introducing sorbent particles modified with lignosulfonates into the exhaust gases.

The present invention is directed to a method for removingsulphur-containing gases from the exhaust gases of a fossil fuel-firedcombustor. In particular, the present method provides for removingsulphur-containing gases by introducing particulate surfactant-modifiedsorbent downstream of the flame zone of the combustor.

BACKGROUND OF THE INVENTION

Relatively costly methods exist for control of sulphur oxide pollutionfrom fossil fuel-fired combustors, but they are most commonly applied tonew facilities where the expense and control of the technology isjustifiable due to the long remaining depreciable lifetime of thefacility. There is a large population of older combustors in existencefor which the cost-effective methods of reducing sulphur oxide emissionsare not generally available due to the substantial additional capitalexpense which would need to be expended on an old facility. There is aneed, therefore, to develop cost-efficient, retrofittable technology tocontrol sulphur oxides and nitrogen oxides in this population of olderplants

In other methods, inorganic promoters have been added to each of thecalcium-based sorbents in an effort to increase their reactivity.Promoters can increase reactivity significantly but each group ofeffective promoters has problems which preclude it from practicalapplication. Transition metals such as chromium are effective in variousforms but they are relatively expensive and may produce environmentalside effects of their own. Alkali metal additives are aggressivepromoters during natural gas-firing, but are condensed on the ash whichis produced during coal-firing and are unavailable to promote SO₂capture by the sorbent. There remains a need in the art, therefore, fora sorbent with an improved capability of capturing SO₂ that will not bedepleted by ash interactions in a coal-fired combustor, and which doesnot introduce detrimental environmental effects.

It is thus an object of the present invention to provide a method forremoving sulpher-containing gases, particularly sulphur oxides, from theexhausts of fossil fuel-fired combustors.

It is also an object of the present invention to provide an improvedsorbent for removing sulphur oxides from the exhaust gases of fossilfuel-fired combustors when said sorbent is injected into, or downstreamfrom the combustor.

These and other objects of the present invention will be apparent fromthe following description and appended claims.

BRIEF DESCRIPTION OF THE DRAWINGS

In accompanying drawings:

FIG. 1 is a graph of the amount of increase in calcium utilization (overunmodified control sorbent) in the sorbent utilized in accordance withthe present invention versus the amount of lignosulfonate concentrationin the sorbent.

FIG. 2 is a graph showing the comparison in the amounts of calciumutilization versus the calcium/sulphur ratio in two sorbents, with andwithout the improvement according to the present invention.

SUMMARY OF THE INVENTION

The present invention provides a method for removing sulphur-containinggases from exhaust gases of fossil fuel-fired combustors comprising thestep of introducing into the exhaust gases sorbent particles capable ofreacting with sulphur oxides wherein the particles comprise calciumhydroxide or calcium magnesium hydroxide and an ionic surfactant. Thesurfactant is preferably an alkali metal lignosulfonate. The sorbentpreferably comprises 1 to 2 percent by weight calcium lignosulfonate butmay contain up to 5 percent by weight calcium lignosulfonate, and ischaracterized by a significantly finer particle size distribution thanthe equivalent sorbent without lignosulfonate.

DESCRIPTION OF THE PREFERRED EMBODIMENT

To practice the method according to the present invention, asurfactant-modified sorbent is prepared. The preferred surfactant is analkali metal lignosulfonate. The sorbent is selected from the groupconsisting of calcium magnesium hydroxide [Ca(OH)₂.Mg(OH)₂ ] and calciumhydroxide [Ca(OH)₂ ].

Initially, limestone (CaCO₃) or dolomite [CaMg(CO₃)₂ ] is calcined toits respective oxide (CaO or CaO.MgO), usually in the temperature rangeof 900° to 1100° C. (lime temperature) but preferably at around 1000° C.This produces a soft-burned lime characteristic of that available atcommercial lime plants. The resulting oxide is then hydrated at a waterto oxide ratio ranging from 2 to 3 but preferably around 2.6, with watercontaining the desired amount of calcium lignosulfonate or other ionicsurfactant. The amount of calcium lignosulfonate utilized will be thatsufficient to produce a resulting calcium hydroxide/calciumlignosulfonate product containing up to about 5 percent by weightcalcium lignosulfonate. Preferably, the resulting product will containabout 1 to 2 percent calcium lignosulfonate.

The calcium lignosulfonate-modified calcium hydroxide sorbent accordingto the present invention results in a higher capture of SO₂ than anunmodified calcium hydroxide when injected into a fossil fuel-firedcombustor or combustor flue system. Typically the modified sorbent willbe injected into the flue where the exhaust gases are at a temperaturein the range of about 65° to 1230° C. Since the improved performance isthe result of a physical rather than a chemical change, the tendency ofcoal ash to remove the enhancement is avoided.

The lignosulfonate-modified sorbents are also improved in that they haveimproved handling characteristics. Commercial hydrates frequently havethe tendencies to cake and agglomerate during storage and handling whichcause problems at their point of use. The lignosulfonate-modifedsorbents according to the present invention are characterized by areduced amount of caking during storage and reduced amount ofagglomeration during handling, thus facilitating handling andcontrollability of fluidization during feeding to the reactor orcombustor.

While not intending to be bound to any particular theory of operation ofthe present invention, it is believed that the surfactant-modifiedsorbents according to the present invention exhibit these improvedproperties, at least in part, because of formation of smaller calciumhydroxide particles. Smaller particles are formed in two ways: (1)during the hydration reaction, surfactant decreases the surface energyof the nucleus/solution interface (surface tension) and therebyincreases the nucleation rate. This results in a large number of smallcrystals rather than a small number of large crystals; (2) the tendencyof small calcium hydroxide crystals to form larger particles throughagglomeration is reduced by eliminating the layer of adsorbed waterwhich surrounds such crystals. This is accomplished by introducing ahydrophobic surfactant layer around the crystals. Thus, both an increasein nucleation rate during the hydration reaction, and a decrease inadsorbed water by enhanced by hydrophobicity of crystal surfaces areeffected by a small quantity of lignosulfonate.

Having described the preferred embodiment of the present invention thefollowing examples are provided for purposes of illustration. However,the examples are not intended to limit the invention in any way.

EXAMPLE 1

A commercially available limestone, Presque Isle, was calcined tocalcium oxide at 1000° C. for 16 hours. A chemical analysis of theresulting lime showed no significant quantities of known inorganicpromoters. The resulting calcium oxide was then hydrated at a water tocalcium oxide ratio of 2.6 with water containing varying amounts ofcalcium lignosulfonate. The amounts of the calcium lignosulfonatesurfactant in the water were calculated to yield 0, 0.5, 1.0, 1.5, 2.0,3.0, 4.0, and 5.0% of calcium lignosulfonate in the product calciumhydroxide. The modified calcium hydroxides were then tested forreactivity with sulphur dioxide in a laboratory scale isothermal flowreactor in which the reactor temperature was held at 1000° C., theresidence time for the reaction was 1 second, and the sulphur dioxideconcentration was 3000 ppm. These are conditions within the range ofthose which would be encountered during downstream injection of asorbent for SO₂ capture in a coal-fired boiler. The increased calciumutilization by the sorbent-containing calcium lignosulfonate over thecontrol sorbent (containing no surfactant) are shown in FIG. 1. At theoptimum calcium lignosulfonate concentrations in the hydroxide (1.5 to2.0 weight percent), calcium utilization increases of approximately 5%absolute (20 to 25% relative) is achieved. With calcium to sulphur ratioof 2 an SO₂ capture of over 60% is calculated.

EXAMPLE 2

Two sorbents were produced for testing in a pilot-scale, coal-firedcombustor. The control sorbent was commercial Longview calciumhydroxide. The modified sorbent was made from commercial Longviewcalcium oxide, experimentally hydrated with water containing calciumlignosulfonate to produce a hydroxide containing 1% calciumlignosulfonate. The sorbent was then injected into a 10⁶ Btu, coal-firedfurnace at 1250° C. The resulting calcium utilizations of the controland modified sorbents are shown in FIG. 2. A 20 to 25% relative increasein calcium utilization by the modified sorbent is shown.

What is claimed is:
 1. A method for removing sulfur oxide sulfuroxide-containing gases from exhaust gases of a fossil fuel-firedcombustor comprising the step of introducing into said exhaust gasessolid particles capable of reacting with said sulfur oxide-containinggases, said particles comprising a surface-modified sorbent selectedfrom the group consisting of alkali metal lignosulfonate-modifiedcalcium hydroxide and alkali metal lignosulfonate-modified calciummagnesium hydroxide, wherein said alkali metal lignosulfonate comprisesup to 5% by weight of the total dry weight of said surface-modifiedsorbent.
 2. The method according to claim 1, wherein said sorbentcomprises calcium hydroxide and said alkali metal lignosulfonatecomprises calcium lignosulfonate.
 3. A method according to claim 2wherein said particles comprise from 1 to 2% calcium lignosulfonate. 4.A method according to claim 3 wherein the particle size distribution ofsaid particles is finer than the distribution of a correspondingnonlignosulfonate modified sorbent.
 5. A method according to claim 2wherein said particles are introduced into said exhaust gases at atemperature in the range of about 65° to 1230° C.